|Publication number||US7419594 B2|
|Application number||US 11/107,946|
|Publication date||Sep 2, 2008|
|Filing date||Apr 15, 2005|
|Priority date||Oct 9, 2003|
|Also published as||CA2542918A1, CA2542918C, US20050178725|
|Publication number||107946, 11107946, US 7419594 B2, US 7419594B2, US-B2-7419594, US7419594 B2, US7419594B2|
|Original Assignee||Shaw Environmental & Infrastructure, Inc.|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (23), Non-Patent Citations (8), Referenced by (3), Classifications (28), Legal Events (6)|
|External Links: USPTO, USPTO Assignment, Espacenet|
This application is a continuation-in-part application of U.S. patent application Ser. No. 10/682,624, filed Oct. 9, 2003, now U.S. Pat. No. 7,018,534, which is incorporated by reference herein in its entirety.
The present invention relates to bioreactors, and more specifically, to the control of biomass growth on suspended media within fluidized-bed bioreactors.
Biological reactors find increasing use in many areas of industry, including waste treatment plants. Efforts to protect the environment include advanced biological treatment of wastewater through the use of biological reactors, and in particular, fluidized-bed bioreactors. It is the activity of biologically active materials (or “biomass”) within the biological reactor that degrades contaminants in the influent to effect a filtration process. As the biomass treats these contaminants through enzymatic reaction, the biomass grows through reproduction within the system. Typically this activity occurs within a treatment vessel which contains media or other substrate material or carriers on which the biomass attaches and grows as contaminants are consumed. Typical media would include plastic beads, resin beads, sand, or ion exchange resins, among other carriers.
Conventional fluidized-bed bioreactors, such as well-mixed suspended carrier reactors (SCRs), suffer from operational limitations in that the media or carriers of the fluidized bed may be subject to excessive buildup of biomass and precipitates, thereby causing compromised flow distribution, excessive media and/or biomass carryover, crusting, increased clogging of filters, and the like. If not properly limited, biomass and precipitate buildup is detrimental to system performance. Uncontrolled biomass film growth in a fluidized bed biological reactor can also result in an undesirable loss of media.
Media bed expansion can, under certain circumstances, be limited by the application of shear, but the success of such a control strategy depends upon whether excess biomass and suspended solids can be transported to the top of the fluidized bed. More specifically, it is recognized that such transportation of excess biomass and suspended solids toward the top of the bed is promoted by several dominant mechanisms. For example, media grains that are coated with thicker layers of biomass tend to have an overall particle density that is less than the average particle density within the fluidized bed. Those particles, therefore, are transported to the top of the fluidized bed by virtue of upward moving fluid flow as well as the reduced particle density. This upward movement results in some shear forces acting on biomass-covered particles which does separate some biomass from its supportive media.
One solution to this problem has been to increase the amount and size of cavities introduced into the system to increase the shear and subsequent separation of the biomass from its media. An example of a bioreactor in which such a system is operated is shown in
The introduction of air into the liquid via air sparger (air inlet) 120 serves two purposes. First, it supplies oxygen which is needed for the enzymatic reactions which are taking place in the system as contaminants are removed and biomass is formed on the media. Secondly, the upward cavity movement causes currents to be developed in the liquid. These currents will cause movement of the media and the application of shear stresses to the media and biomass. This interaction between pieces of media with other pieces of media, fluid, biomass, and the interior wall(s) of vessel 100 results in collisions which cause: (1) contact between the microorganisms and suspended organic matter, and (2) accumulated biomass to break free from its respective supportive media. This freed biomass will typically rise to the top of the vessel as its density is less than that of the liquid system.
Many of these types of systems rely on the filtering of treated effluent (e.g. purified water in the case of waste water treatment) at filter 140 to remove clean product water or to separate the bioreactor media from the effluent. This leads to shut-down time and other expensive aspects to the operation of the reactor. As product water is drawn off and fresh waste feed is caused to flow into the reactor, it becomes necessary to remove resultant biomass. With too great a biomass concentration in the reactor, filter fouling, plugging, excessive biomass in the effluent and other problems compound to affect the reactor performance.
Thus, there remains a need in the industry for an improved system for removing accumulated biomass from a slurry of a fluidized-bed bioreactor to inhibit uncontrolled biomass growth and precipitate accumulation. Objects and advantages of the invention will become apparent to those skilled in the art from the drawings, the detailed description of preferred embodiments, and the appended claims.
The present invention provides a bioreactor comprising a vessel configured to contain an aqueous suspension of biomass and media. The invention includes a lift tube disposed within the vessel, the lift tube having an inlet disposed at the bottom region of the vessel and an outlet disposed at the top region of the vessel. A gas inlet is positioned to feed gas into the lift tube, optionally at a location proximal to the inlet of the lift tube. The gas inlet is configured to introduce a stream of gas to promote separation of the biomass from the media in the lift tube. An adjustable weir is disposed proximal to the outlet of the lift tube, the weir being adjustable between a lower position and a higher position. Means for removing biomass from the weir are provided in fluid communication with the weir, and the weir height is adjustable to control the removal of biomass from the vessel.
Also included as a part of the invention is a method for controlling the removal of biomass in a bioreactor containing a lift tube with an inlet and outlet. The method comprises the steps of introducing a stream of gas into an inlet of a lift pipe to generate sufficient shear forces to separate biomass from the media, disposing a weir proximal the outlet of the lift tube in fluid communication with a point external to the bioreactor, and adjusting the height of the weir to thereby control the removal of biomass from the bioreactor.
Another embodiment of the present invention is a bioreactor comprising a vessel configured to contain an aqueous suspension of biomass and media, a lift tube disposed within the vessel, the lift tube having an inlet disposed at the bottom region of the vessel and an outlet disposed at the top region of the vessel, a gas inlet positioned to feed gas into the lift tube, where the gas inlet is configured to introduce a stream of gas to promote separation of the biomass from the media in the lift tube, and a quiescent zone disposed proximate the lift tube inlet.
Still another embodiment is a bioreactor comprising a vessel configured to contain an aqueous suspension of biomass and media, a gas inlet at the bottom region of the vessel positioned radially outward from the geometric center of the vessel, a barrier disposed within the vessel between the gas inlet and the geometric center of the vessel, the barrier being positioned to allow the passage of the aqueous suspension of biomass and media both under and over the barrier whereby a fluid loop is formed within the vessel around the barrier when the gas inlet is introducing gas into the vessel, and a quiescent zone disposed at the bottom region of the vessel proximate the geometric center of the vessel.
Still yet another embodiment includes a bioreactor comprising a vessel configured to contain an aqueous suspension of biomass and media, a first gas inlet at the bottom region of the vessel, the first gas inlet positioned radially outward from the geometric center of the vessel, a barrier disposed within the vessel between the first gas inlet and the geometric center of the vessel, the barrier being positioned to allow passage of the aqueous suspension of biomass and media both under and over the barrier whereby a fluid flow loop is formed within the vessel around the barrier when the first gas inlet is introducing gas into the vessel, and a lift tube disposed within the vessel, the lift tube having an inlet disposed at the bottom region of the vessel and an outlet disposed at the top region of the vessel. Included in this embodiment is a second gas inlet positioned to feed gas into the lift tube, the second gas inlet being configured to introduce a second stream of gas to promote separation of the biomass from the media in the lift tube.
In yet still another embodiment, a bioreactor comprises a vessel configured to contain an aqueous suspension of biomass and media, a gas inlet at the bottom region of the vessel, the gas inlet positioned radially outward from the geometric center of the vessel, a barrier disposed within the vessel between the gas inlet and the geometric center of the vessel, the barrier being positioned to allow the passage of the aqueous suspension of biomass and media both under and over the barrier whereby a fluid loop is formed within the vessel around the barrier when the gas inlet is introducing gas into the vessel, and collection baffles disposed above the gas inlet configured to allow at least a portion of the media to fall toward the bottom region of the vessel without being entrained in a gas stream when the gas inlet is introducing gas into the vessel.
The invention is best understood from the following detailed description when read in connection with the accompanying drawings. It is emphasized that, according to common practice, the various features of the drawings are not to scale. On the contrary, the dimensions of the various features are arbitrarily expanded or reduced for clarity. Included in the drawings are the following figures:
This invention will now be described with reference to several embodiments selected for illustration in the drawings. It will be appreciated that the scope and spirit of the invention are not limited to the illustrated embodiments. It will further be appreciated that the drawings are not rendered to any particular proportion or scale. Also, any dimensions referred to in the description of the illustrated embodiments are provided merely for the purpose of illustration. The invention is not limited to any particular dimensions, materials, or other details of the illustrated embodiments.
As discussed above, typical air sparging which would occur in a fluidized-bed bioreactor achieves two effects. It introduces oxygen needed for enzymatic reaction and also causes mixing and interaction within the system between system components. This intended mixing aids in oxygen mass transfer (the first effect), as well as biomass growth control through the introduction of shear forces via turbulent flow interaction between media and other parts of the system.
The delivery of gas into lift tube 200 causes the rise of cavities 110 within the lift tube. This causes upward flow of fluid within the lift tube as the fluid and biomass-covered media are entrained in the rising fluid. This movement, along with the movement of the cavities themselves, causes shear forces to operate on the biomass media and the biomass carried thereon and thereby causes the separation of biomass 240 from the biomass media. As the biomass 240 becomes separated from the media, it accumulates in the region just above the lift tube, as shown in
More specifically, and as shown in
Another aspect of the present invention is the use of the disclosed apparatus in a novel method for achieving efficient bioreactions through careful biomass concentration control within the bioreactor. A preferred method generally comprises the steps of introducing a stream of gas into a bioreactor (e.g. near an inlet of a lift pipe) to generate sufficient shear forces to separate biomass from media, disposing a weir proximal the outlet of the lift tube in fluid communication with a point external the bioreactor, and adjusting the height or elevation of the weir to thereby control the removal of biomass from the bioreactor.
Preferably, the method operates by passing air into the bioreactor, although oxygen enriched air or even pure oxygen could be used. In a typical application of the present method, the bioreactor is used to treat waste water, whereby a stream of contaminated water or sewage is introduced into the vessel and, after sufficient enzymatic activity is allowed to occur, a purified water stream from the bioreactor is removed via effluent removal pipe 270.
Other exemplary features of an embodiment of the invention are shown in
Because lift tube 200, in conjunction with its gas inlet line 210, causes an upward flow of fluid and resultant upward movement of media and biomass which is entrained in the upward moving fluid, a fluid flow, or current, is developed within the system as shown by the arrows in
Aiding in the settlement of media in quiescent zone 600 are lift loops shown by arrows indicating fluid flow in
The idea is that, no matter the shape or configuration of the vessel and barrier, the barrier according to this embodiment is disposed radially between the lift tube and gas inlets so as to provide for a fluid flow loop whereby fluid flows upward outside of the barrier and downward inside the barrier, as shown by the arrows indicating flow in
Also shown in
Included as a part of the present invention is the use of the various apparatus in novel methods for achieving efficient bioreactions through careful biomass concentration control within the bioreactor. In addition to the method described above, another preferred method generally comprises the steps of introducing a stream of gas into a bioreactor near an inlet of a lift pipe to generate sufficient shear forces to separate biomass from the media, and generating at least one flow loop within the bioreactor to allow for media settlement within a quiescent zone disposed near the bottom center of the bioreactor, whereby the quiescent zone feeds biomass covered media to the bottom of the lift tube. A preferred means of generating the flow loop is the use of a barrier and a gas inlet (separate from the lift tube gas inlet) to create a lift loop for upward fluid flow between the barrier and vessel wall.
Also included is a method of generating a cleaned effluent stream comprising the steps of introducing a stream of gas into a bioreactor below at least one collection baffle, and removing a cleaned effluent stream above the collection baffles, whereby entrained media and/or biomass is prevented from entering the area of the bioreactor where effluent product is removed.
Still other methods of using the various disclosed embodiments, including specific combinations thereof, could be envisioned by one skilled in the art with the benefit of the foregoing. These and other methods are considered a part of the present invention.
Although preferred embodiments of the invention have been shown and described herein, it will be understood that such embodiments are provided by way of example only. Numerous variations, changes and substitutions will occur to those skilled in the art without departing from the spirit of the invention. Accordingly, it is intended that the appended claims cover all such variations as fall within the spirit and scope of the invention.
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US2024986 *||May 5, 1932||Dec 17, 1935||Chicago Pump Co||Apparatus for and method of sewage treatment|
|US2638444 *||Aug 2, 1949||May 12, 1953||Kappe Stanley E||Sewage digester|
|US3043433 *||May 17, 1961||Jul 10, 1962||Caton Singer Oscar||Sewage treatment plant|
|US3152982 *||Jan 24, 1963||Oct 13, 1964||Ross Pagnotti Joseph||Method and apparatus for sewage treatment|
|US3182801 *||May 22, 1962||May 11, 1965||Coleman Griffith Charles||Sewage treatment tank with aeration chamber and settling chamber|
|US3224964 *||Apr 3, 1961||Dec 21, 1965||Fuller Co||Apparatus and process for biological purification of waste water containing foam forming substances|
|US4137171||May 3, 1974||Jan 30, 1979||Ishigaki Kiko Co., Ltd.||Process for treating waste water and an apparatus therefor|
|US4452701||Nov 4, 1982||Jun 5, 1984||Garrett Michael E||Biological treatment of sewage|
|US4454038||Oct 31, 1980||Jun 12, 1984||Chiyoda Chemical Engineering And Construction Co., Ltd.||Apparatus for biological treatment of waste water in downflow operation|
|US4521311||Jul 29, 1983||Jun 4, 1985||Linde Aktiengesellschaft||Activated sludge system with integrated regenerator|
|US4810377||Sep 10, 1987||Mar 7, 1989||Kabushiki Kaisha Iseki Kaihatsu Koki||Clarification device|
|US4839053||Sep 30, 1987||Jun 13, 1989||Ashbrook-Simon-Hartley Corp.||Biomass growth process with separate aeration and media compartments|
|US5372712||Feb 25, 1993||Dec 13, 1994||Envirex Inc.||Biomass growth control apparatus for fluid bed biological reactor|
|US5942116 *||Aug 1, 1997||Aug 24, 1999||Clark; Sidney E.||Anaerobic sludge digester|
|US6077424||May 23, 1996||Jun 20, 2000||Ebara Corporation||Method for aerobically treating wastewater and a treatment tank for such method|
|US6168717 *||Jan 20, 1999||Jan 2, 2001||Thermal Process Systems, Llc||Process for controlling foam in a treatment reactor|
|US6616845||May 29, 2001||Sep 9, 2003||Aqwise Wise Water Technologies, Ltd.||Method and apparatus for biological wastewater treatment|
|JP2000167579A||Title not available|
|JP2002079283A||Title not available|
|JP2003154385A||Title not available|
|JP2003300086A||Title not available|
|JPH10244295A||Title not available|
|WO2005034613A2||Oct 8, 2004||Apr 21, 2005||Shaw Environmental & Infrastructure, Inc.||Apparatus and method for controlling biomass growth in suspended carrier bioreactor|
|1||Combined British Search and Examination Report corresponding to GB0607540.2 dated Jun. 30, 2006.|
|2||Eckenfelder, "Principles of Water Quality Management", 1980, pp. 216 and 218.|
|3||Search Report for claim 19, application No. GB0607540.2, dated Dec. 14, 2006.|
|4||Search Report for claim 20, application No. GB0607540.2, dated Dec. 15, 2006.|
|5||Search Report for claim 21, application No. GB0607540.2, dated Dec. 15, 2006.|
|6||Search Report for claim 22, application No. GB0607540.2, dated Dec. 15, 2006.|
|7||Steel and McGhee, "Water Supply and Sewerage", 1979, pp. 503, 508 and 509.|
|8||*||Translation of Japanese patent 10-244295, Sep. 1998.|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US8551341 *||Jun 15, 2010||Oct 8, 2013||Saudi Arabian Oil Company||Suspended media membrane biological reactor system including suspension system and multiple biological reactor zones|
|US20110017664 *||Jun 15, 2010||Jan 27, 2011||Conner William G||Suspended media membrane biological reactor system and process including suspension system and multiple biological reactor zones|
|US20120155974 *||Jan 19, 2010||Jun 21, 2012||Bryan Jr Vincent E||Decelerator comprising deceleration tank and extraction conveyor|
|U.S. Classification||210/608, 210/220, 210/629, 210/197, 210/620, 210/540|
|International Classification||B01D33/80, C02F3/02, C02F3/08, C02F3/22, B01D35/00, B01D33/70, C02F3/12, C02F3/00, C02F9/00, A01K|
|Cooperative Classification||Y02W10/15, C12M27/24, C12M29/08, C02F1/24, C02F3/223, C02F3/085, C02F3/26, C02F3/087|
|European Classification||C02F3/08D, C02F3/26, C02F3/08D2, C02F3/22C|
|Apr 15, 2005||AS||Assignment|
Owner name: SHAW ENVIRONMENTAL & INFRASTRUCTURE, INC, NEW JERS
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:FRISCH, SAMUEL;REEL/FRAME:016482/0433
Effective date: 20050330
|Jul 10, 2009||AS||Assignment|
Owner name: BASIN WATER, INC., CALIFORNIA
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:SHAW ENVIRONMENTAL & INFRASTRUCTURE, INC.;ENVIROGEN, INC.;REEL/FRAME:022939/0350
Effective date: 20080918
Owner name: BASIN WATER, INC.,CALIFORNIA
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:SHAW ENVIRONMENTAL & INFRASTRUCTURE, INC.;ENVIROGEN, INC.;REEL/FRAME:022939/0350
Effective date: 20080918
|Aug 31, 2010||AS||Assignment|
Owner name: ENVIROGEN TECHNOLOGIES, INC., NEW JERSEY
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:BASIN WATER, INC.;REEL/FRAME:024915/0109
Effective date: 20090715
|Feb 15, 2012||FPAY||Fee payment|
Year of fee payment: 4
|Mar 1, 2016||FPAY||Fee payment|
Year of fee payment: 8
|May 27, 2016||AS||Assignment|
Owner name: HSBC BANK PLC, UNITED KINGDOM
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:ENVIROGEN TECHNOLOGIES, INC.;REEL/FRAME:038735/0602
Effective date: 20160527